TWO-STAGE CATALYST FOR REMOVAL OF NOx FROM EXHAUST GAS STREAM
US-2018283251-A1 · Oct 4, 2018 · US
US10857504B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10857504-B2 |
| Application number | US-201916435773-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 10, 2019 |
| Priority date | Mar 31, 2017 |
| Publication date | Dec 8, 2020 |
| Grant date | Dec 8, 2020 |
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A co-catalyst system for the removal of NO x from an exhaust gas stream has a layered oxide and a spinel of formula Ni 0.15 Co 0.85 CoAlO 4 . The system converts to nitric oxide to nitrogen gas with high product specificity. The layered oxide is configured to convert NO x in the exhaust gas stream to an N 2 O intermediate, and the spinel is configured to convert the N 2 O intermediate to N 2 .
Opening claim text (preview).
What is claimed is: 1. A catalytic converter for the removal of NO x from an exhaust gas stream operating between 350 and 550° C., the catalytic converter comprising: an inlet configured to receive the exhaust gas stream into an enclosure; an outlet configured to allow the exhaust gas stream to exit the enclosure; and a co-catalyst system contained inside the enclosure, the co-catalyst system having: a layered oxide having a formula La 2-x M x QO 4 , for catalyzing a reduction reaction of at least one of NO and NO 2 to generate N 2 O wherein: M is a cationic metal selected from the group consisting of: Ca, Sr, Ba, and a combination thereof; Q is a cationic metal selected from the group consisting of: Fe, Ni, Co, and a combination thereof; and a spinel having a formula, Ni y Co 1-y CoAlO 4 , wherein y is a value within a range of about 0.1 to about 0.9, inclusive, for catalyzing a decomposition reaction of N 2 O to N 2 . 2. The catalytic converter according to claim 1 , wherein the co-catalyst system is configured as a sequential co-catalyst and the exhaust gas stream moves in a flow direction, with the layered oxide being positioned upstream of the spinel structure relative to the flow direction. 3. The converter according to claim 1 , further comprising a separation space between the first chamber and the second chamber. 4. The catalytic converter according to claim 1 , wherein the co-catalyst system is configured as a mixed co-catalyst in which the layered oxide and the spinel are substantially intermixed. 5. The catalytic converter according to claim 1 , wherein the layered oxide comprises LaBaCoO 4 . 6. The catalytic converter according to claim 1 , wherein the layered oxide comprises LaBaFeO 4 . 7. The catalytic converter according to claim 1 , wherein the layered oxide is in a nanoparticle form, of 2 to 50 nm in diameter. 8. The catalytic converter according to claim 1 , wherein the spinel has a formula, Ni 0.15 Co 0.85 CoAlO 4 . 9. The catalytic converter according to claim 1 , wherein the spinel is in nanoparticle form, of 2 to 50 nm in diameter. 10. A two-stage method for the removal of NO x from an exhaust gas stream, the method comprising: flowing the exhaust gas stream through a co-catalyst system comprising: exposing the exhaust gas stream to a layered oxide and catalyzing a reduction of at least one of NO and NO 2 to generate N 2 O, the layered oxide having a formula La 2-x M x QO 4 , wherein: M is a cationic metal selected from the group consisting of: Ca, Sr, Ba, and a combination thereof; Q is a cationic metal selected from the group consisting of: Fe, Ni, Co, and a combination thereof; and x is within a range of from about 0.01 to about 1.5, inclusive; and contacting the exhaust gas stream with a spinel having a formula Ni y Co 1-y CoAlO 4 , wherein y is a value within a range of about 0.1 to about 0.9, inclusive, to decompose the N 2 O to N 2 . 11. The method as recited in claim 10 , wherein the layered oxide comprises at least one of LaBaFeO 4 and LaBaCoO 4 . 12. The method as recited in claim 10 , comprising exposing the exhaust gas stream to the layered oxide prior to exposing the exhaust gas stream to the spinel. 13. The method as recited in claim 10 , comprising flowing the exhaust gas stream through the co-catalyst at a temperature less than about 500° C. 14. The method as recited in claim 10 , comprising recirculating the exhaust gas stream through the co-catalyst system.
Compounds characterised by their crystallite size · CPC title
Nanoparticles · CPC title
Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties · CPC title
X-ray diffraction · CPC title
characterised by their crystalline properties, e.g. semi-crystalline (catalysts comprising carbon B01J21/18; molecular sieves B01J29/00) · CPC title
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